Heat sink and method for producing the same

文档序号:1676920 发布日期:2019-12-31 浏览:21次 中文

阅读说明:本技术 散热器和用于生产该散热器的方法 (Heat sink and method for producing the same ) 是由 J·科迪 L·沃维肯 于 2018-05-18 设计创作,主要内容包括:本发明涉及一种散热器(100),所述散热器包括设有多个流体流动通道的基本上平坦的实心板(101),所述多个流体流动通道形成为将冷却剂从所述板的入口(110)引导至出口(120),其中,所述多个通道包括至少两个主通道(10、20),所述至少两个主通道通过至少多个桥接通道(31-34、36-37)互连,所述至少多个桥接通道在它们各自的附连至所述主通道的点之间没有进一步分支,其中,所述桥接通道(31-34、36-37)具有沿流动方向局部增大的横截面,并且其中,所述桥接通道(31-34、36-37)具有沿流动方向在所述横截面局部增大的下游局部减小的横截面。本发明还涉及一种用于制造散热器的方法。(The invention relates to a heat sink (100) comprising a substantially flat, solid plate (101) provided with a plurality of fluid flow channels, the plurality of fluid flow channels are formed to direct coolant from an inlet (110) to an outlet (120) of the plate, wherein the plurality of channels comprises at least two main channels (10, 20) interconnected by at least a plurality of bridge channels (31-34, 36-37), the at least a plurality of bridge channels are free from further branching between their respective points of attachment to the main channel, wherein the bridge channels (31-34, 36-37) have a cross section which locally increases in the flow direction, and wherein, the bridge channels (31-34, 36-37) have a locally decreasing cross section downstream of the locally increasing cross section in the flow direction. The invention also relates to a method for manufacturing a heat sink.)

1. A heat sink (100) comprising a substantially flat, solid plate (101) provided with a plurality of fluid flow channels formed to direct coolant from an inlet (110) to an outlet (120) of the plate,

wherein the plurality of channels comprises at least two main channels (10, 20) interconnected by at least a plurality of bridge channels (31-34, 36-37) without further branching between their respective points of attachment to the main channels;

wherein the bridge channels (31-34, 36-37) have a cross section which locally increases in the flow direction; and is

Wherein the bridge channel (31-34, 36-37) has a locally decreasing cross section downstream of the locally increasing cross section in the flow direction.

2. A heat sink (100) according to claim 1, wherein the main channel (10, 20) has a smallest cross-section larger than the largest cross-section of its bridging channel (31-37).

3. Radiator (100) according to any one of the preceding claims, wherein the main channel (10, 20) travels along a substantially straight trajectory over a distance of at least 1/3 times, preferably at least 1/2 times, more preferably at least 2/3 times, or most preferably even at least 3/4 times the length of the external dimension of the radiator (100) in the flow direction.

4. A heat sink (100) according to any of the preceding claims, wherein the local increase in cross-section starts from a connection point with one of the main channels (10) upstream of the bridge channel (31-37).

5. The heat sink (100) according to any of the preceding claims, wherein the portions of the solid plates remaining between the fluid flow channels form islands not exhibiting multiple axes of symmetry, and wherein different island shapes occur.

6. The heat sink (100) according to any of the preceding claims, wherein the inlet (110) and/or the outlet (120) are arranged on the circumference of the plate (101).

7. The heat sink (100) according to any of the preceding claims, wherein the plurality of fluid flow channels have a common minimum width.

8. Heat sink (100) according to any of the preceding claims, characterised in that the substantially flat, solid plate (101) is provided with a cover (102) on the surface of one of its main faces, which cover is fixed by means of connection means engaging with the plate material present between the channels.

9. A method of manufacturing a heat sink (100) according to any of the preceding claims, the method comprising:

-cutting a substantially flat solid sheet (101) from a quantity of raw material;

-machining the plurality of flow channels to a depth of less than the total thickness of the substantially flat, solid plate, such that the plurality of channels comprises at least two main channels (10, 20) interconnected by at least a plurality of bridge channels (31-37), and such that the bridge channels have a locally increasing cross-section in the flow direction; and

-placing a substantially flat cover (102) onto the machined plate (101).

Technical Field

The invention relates to the field of radiators.

Background

A heat sink is a physical structure that transfers heat generated by another device to a fluid medium, which is then directed away from the device.

Cooling of components is a recurring problem in the industry. The reason for this is that the lifetime of the components is often strongly dependent on the operating temperature. Thus, active cooling is applied to the component in an attempt to keep the maximum temperature below a certain limit temperature. Examples of such components include from lasers to motors and power electronics. Furthermore, the product may require cooling during production. This is the case, for example, for casting. By applying active cooling during casting, the cycle time is reduced, with a consequent increase in productivity. However, insufficient cooling can result in reduced product quality.

A liquid-cooled plate is essentially a heat sink through which a liquid coolant flows. Various heat sources are mounted on the cooling plate. A common design of such common cooling plates is a metal plate with one serpentine cooling channel that extends over all heat sources. However, in conventional serpentine heat sinks, the fluid heats up along the serpentine channel, which adversely affects cooling near the ends of the channel.

The doctor's paper by van Oevelen (KU Leuven, 11 months 2014) "Optimal Heat Sink Design for Liquid Cooling of electronic devices (Optimal Heat Sink Design for Liquid Cooling of Electronics)" developed an advanced numerical Design method for micro Heat sinks. Two approaches are discussed: shape optimization of individual microchannels and topology optimization of heat sinks. The topology optimization problem is solved by optimally controlling the fictive porosity used to distinguish solid materials from fluids in the two-dimensional model used. Although this work theoretically improves serpentine heat sinks, for example in terms of reducing thermal gradients, the possibility of using a model in which the "solid" portion of the plate is porous and of using substantially infinite narrow channels makes the results impractical for real world manufacturing.

German patent application publication DE102011118483a1 in the name of Volkswagen DE discloses a heat exchanger comprising a housing oriented in a longitudinal direction from a front side to a rear side. The structured transfer surface of the solid part has a flat base surface with mutually spaced transfer elements. The transfer element is aligned parallel to the protrusion of the base. The oriented cross-sections of the base are set to have different widths perpendicular to the longitudinal direction and different lengths parallel to the longitudinal direction, such that the maximum length has a greater extension than the maximum width.

U.S. patent application publication No. US2014/091453a1, assigned to TOYOTA JIDOSHOKKI KK, discloses a cooling device including a base and a plurality of heat sink fins. The base includes an exterior, an interior, an inlet, and an outlet. The heating element is connected to the outside of the base. The heat sink fins are located adjacent to the heat generating element inside the base. The heat sink is arranged from the inlet to the outlet. Each radiator has a lateral cross section having a dimension in a flow direction of the cooling medium and a dimension in a transverse direction perpendicular to the flow direction of the cooling medium. The dimension in the flow direction is longer than the dimension in the transverse direction. The heat sink fins are separated from each other by a predetermined distance in the lateral direction.

U.S. patent application publication No. US2009/145581a1 in the name of Paul Hoffman et al discloses a non-linear fin heat sink for uniformly dissipating/removing heat from a device where the heat generated across the device is non-uniform while also providing a small and relatively lightweight heat sink. The heat sink having extended surface protrusions optimally shaped as described in the identification of convective heat transfer, conductive heat transfer and flow resistance, thereby allowing the heat sink to counteract a temperature rise of the coolant medium and provide enhanced cooling of the coolant temperature, delivering optimal cooling efficiency according to local physical properties of the coolant medium, for use with a fluid to achieve heat transfer; either a liquid coolant, a gaseous coolant, or a combination thereof. In addition, heat sinks are characterized by an array of fins through which the coolant flow passes to enhance turbulence of the coolant flow, such an array of fins being characterized by non-linear shapes, spacing and height patterns to provide optimal cooling while reducing volume and flow resistance.

Article "TCPT-2006-096. R2: a Micro Scale pin fin Heat sink-parameter Performance evaluation study (Micro Scale pin fin Heat Sinks-Parametric Performance evaluation study), reported by the institute of electrical and electronics engineers for component and packaging technology, volume 30, No. 4, proposes an experimentally conducted Parametric study of Heat transfer and pressure drop associated with forced flow of deionized water over five Micro pin fin Heat Sinks of different spacing, arrangement and shape. Nusselt numbers and coefficients of friction are obtained in the Reynolds number range 14-720. Thermal and hydraulic results were obtained to evaluate and compare radiator performance at a fixed mass flow rate, a fixed pressure drop, and a fixed pumping power. For non-streamlined pin fin devices, two different reynolds number dependent nussel regions separated by a critical reynolds number have been identified, whereas streamlined devices show no slope variation. The effect of the spacing, shape and arrangement of pin fins on the coefficient of friction and heat transfer is consistent with the prior art. The results show that the use of a streamlined pin fin radiator can significantly improve the thermo-hydraulic performance of the radiator, but only at moderate reynolds numbers.

Existing solutions do not appear to provide a satisfactory compromise between thermal efficiency and pressure drop. Accordingly, there remains a need for improved heat sinks.

SUMMARY

Embodiments of the present invention propose a new cooling solution, implemented by topology optimization, for use mainly in industrial settings.

According to an embodiment of the invention, there is provided a heat sink comprising a substantially flat solid plate provided with a plurality of fluid flow channels formed to guide coolant from an inlet to an outlet of the plate, wherein the plurality of channels comprises at least two main channels interconnected by at least a plurality of bridge channels which are not further branched between their respective points of attachment to the main channels, wherein the bridge channels have a cross-section which locally increases in the flow direction, and wherein the bridge channels have a cross-section which locally decreases downstream of the local increase in the cross-section in the flow direction.

The term "plate" is used to refer to a plate-like structure having substantially parallel top and bottom surfaces and a peripheral edge whereby the top and/or bottom surfaces are brought into contact with a heat source from which heat is to be removed. The peripheral edges generally define a rectangular shape, although other polygonal and non-polygonal shapes may be preferred depending on the application.

The term "main channel" is used herein to denote a channel section interconnected by other channels. A heat sink according to the present invention may have two or more primary channels that typically, but not necessarily, exhibit some symmetry in their construction.

In the sense of the claimed invention, some or all of the channels interconnecting a pair of main channels may be considered "bridging channels", which means that they are provided with a locally increasing cross-section in the flow direction and a locally decreasing cross-section downstream of said local increase in cross-section in the flow direction, and that they are not further branched between their respective points of attachment to the main channels.

The present invention is based primarily on the surprising insight of the inventors that by providing bridging channels with a locally increased cross-section in the flow direction, a more optimal balance between pressure drop and fluid flow can be achieved. Since the allowable pressure drop is typically dictated by external conditions (e.g., the characteristics of the coolant pump to be used), maximizing fluid flow (and thus heat transfer) of the heat sink for that particular given pressure is a highly desirable characteristic. Although the literature suggests, based on theoretical considerations, the use of channels that narrow in the direction of flow, surprisingly good flow rates have been obtained by violating this suggestion and using bridging channels that exhibit locally widening stages.

Furthermore, the bridge channels narrow again downstream of the restriction before reaching the main channel towards which they convey the fluid. The inventors have found that this arrangement allows bridging a wider "mid-section" of the channel, which reduces the pressure drop across the channel. In particular, the combination of a wider "mid-section" and restrictions at the inflow and outflow portions of the bridging channel allows for an optimal design compromise between pressure drop over the channel and heat rejection efficiency.

In an embodiment of the heat sink according to the invention, the main channel has a smallest cross-section which is larger than a largest cross-section of its bridging channel.

In an embodiment of the heat sink according to the invention, the main channel travels along a substantially straight trajectory over a distance of at least 1/3 times, preferably at least 1/2 times, more preferably at least 2/3 times, or most preferably even at least 3/4 times the length of the outer dimension of the heat sink in the flow direction.

The main channel may be composed of several substantially straight sections having a basic length, for example a length satisfying the minimum lengths listed above.

These arrangements allow for a design in which the main channels define the total flow of cooling fluid through the plate, whereby the bridging channels locally regulate the amount of heat that can be absorbed and rejected per unit area.

In an embodiment of the heat sink according to the invention the local increase in cross-section starts from a connection point with one of the main channels upstream of the bridge channel.

In this embodiment, the bridge channels exhibit cross-sectional restrictions at the point where they connect to the main channel from which they receive their flow. The inventors have found that this limitation is a particularly effective feature of adjusting the mass flow rate through such bridging channels, thereby improving heat exchange and heat rejection at these points.

In an embodiment of the heat sink according to the invention, the portions of the solid plates remaining between the fluid flow channels form islands which do not exhibit a plurality of axes of symmetry, and wherein different island shapes occur.

In this embodiment, the islands (also referred to as "fins") show some geometric variation, allowing for variation in heat transfer characteristics along the overall path of the cooling fluid.

In an embodiment of the heat sink according to the invention, the inlet and/or the outlet are arranged on the circumference of the plate.

Although it is equally possible to have inlets and/or outlets on the main face of a substantially flat solid plate, the advantage of providing inlets and/or outlets on the circumference is that the entire heat sink remains substantially flat, allowing for a more efficient use of space, the available mounting height of which is limited.

In an embodiment of the heat sink according to the invention, the plurality of fluid flow channels have a common minimum width.

An advantage of this embodiment is that it allows for the production of multiple channels in a plate by the same industrial process. For example, a common minimum width of 0.1mm makes the channels suitable for production by CNC milling or the like, whereas a common minimum width of 0.5mm can be obtained by metal printing with SLM.

In an embodiment of the heat sink according to the invention, the substantially flat, solid plate is provided with a cover on a surface of one of its main faces, the cover being fixed by means of a connecting means engaging with the plate material present between the plurality of channels.

An advantage of this embodiment is that it allows manufacturing of a plate with a plurality of channels by known industrial processes such as CNC milling, wherein the channels are closed at their open ends by a cover. Since the connecting means, which may comprise conventional connectors, such as screws or bolts, but may also comprise adhesives and welding, engage the sheet material present between the channels, the cooling efficiency is not disturbed.

According to an aspect of the present invention, there is provided a method of producing the heat spreader as described above, the method comprising: cutting a substantially flat solid sheet from a quantity of stock material; machining the plurality of flow channels to a depth of less than the total thickness of the substantially flat, solid plate such that the plurality of channels comprises at least two main channels interconnected by at least a plurality of bridge channels, and such that the bridge channels have a locally increasing cross-section in the flow direction; and placing a substantially flat cover onto the processed plate.

The technical effects and advantages of the embodiments of the method according to the invention correspond, mutatis mutandis, to those of the corresponding embodiments of the heat sink according to the invention.

Brief description of the drawings

These and other features and advantages of embodiments of the present invention will now be described in more detail, with reference to the accompanying drawings, in which:

figure 1 shows a two-dimensional image of a first embodiment of a heat sink according to the invention;

figure 2 shows a two-dimensional image of a first embodiment of a heat sink according to the invention;

figure 3 shows a two-dimensional image of a third embodiment of a heat sink according to the invention;

figure 4 shows an exemplary heat sink with a serpentine flow channel known in the prior art; and

fig. 5 shows a flow chart of an embodiment of the method according to the invention.

Description of the embodiments

As mentioned above, a heat sink is a physical structure that transfers heat generated by another device to a fluid medium (hereinafter also referred to as "coolant"), which is then directed away from the device. A liquid-cooled plate is essentially a heat sink through which a liquid coolant flows. The heat transfer is affected by the flow characteristics of the coolant through the channels of the liquid cooling plate (e.g., whether the flow is laminar or turbulent), which will depend on the geometry of the channels, the nature of the coolant, and the flow rate. Efficient heat transfer is obtained by convection in the coolant.

The inventors have found that certain novel designs of the liquid channels of the cooling plate are better at meeting certain criteria, such as reduced thermal expansion, lower maximum temperature, more uniform surface temperature, etc. The design according to the invention may be adapted to meet relevant constraints such as assembly constraints (screws), manufacturing constraints, structural integrity and limited pressure drop.

In general, the desired variation in channel cross-section for the present invention can be achieved by varying the width and/or depth of the channel. Since the present description refers to two-dimensional figures, all variations in cross-section are assumed to be obtained by variations in width only; this is for clarity purposes only and without loss of generality.

Fig. 1 shows a two-dimensional image of a first embodiment of a heat sink according to the present invention.

The heat sink 100 comprises a substantially flat solid plate provided with a plurality of fluid flow channels. A plurality of fluid flow channels are formed to direct coolant from the inlet 110 to the outlet 120 of the plate. In this embodiment, the plate is bounded peripherally by an impermeable edge, and the inlet 110 and outlet 120 are interruptions in said edge through which the coolant can enter and exit the radiator 100, respectively. Since the inlet 110 and the outlet 120 are arranged on opposite sides of the plate 101, the coolant travels through the plate substantially from left to right.

The plurality of channels comprises at least two main channels 10, 20 which are interconnected by at least a plurality of bridge channels 31-34 and 35-37. The skilled person will observe the symmetry of the arrangement of fig. 1 around a central horizontal axis; the pairing of the main channel 20 and the bridge channels 31-37 in the lower half of fig. 1 is not numbered in order to keep the drawing and the description concise, but their operation is of course the same.

The bridge channels 31-34 and 36-37 have a cross section which locally increases in the flow direction, i.e. in the direction from the main channel 10 towards the main channel 20 in the figure. In practice it can be seen that the local increase in cross-section starts from the connection point with the main channel 10 upstream of the bridge channels 31-34 and 36-37, forming a restriction at or near said connection point.

It can also be seen that the bridging channels 31-34 and 36-37 are not branched and that they have a locally decreasing cross-section downstream of the locally increasing cross-section in the flow direction. This appears as a second restriction located near the junction of the main channel 20 downstream of the bridge channels 31-34 and 36-37.

Fig. 2 shows a two-dimensional image of a second embodiment of a heat sink according to the present invention.

The heat sink 100 comprises a substantially flat solid plate 101, said solid plate 101 being provided with a plurality of fluid flow channels. A plurality of fluid flow channels are formed to direct coolant from the inlet 110 to the outlet 120 of the plate. In this embodiment the plate is bounded peripherally by impermeable edges, and the inlet 110 and outlet 120 are arranged on the circumference of the plate 101 and provided with attachment points for fluid ducts or the like. Since the inlet 110 and the outlet 120 are arranged on opposite sides of the plate 101, the coolant travels through the plate substantially from left to right.

The plurality of channels comprises at least two main channels 10, 20 'which are interconnected by at least a plurality of bridging channels 31, 31'. The skilled person will observe the symmetry of the arrangement of fig. 1 around a central horizontal axis.

The bridge channels 31, 31 'have a cross-section which locally increases in the flow direction, i.e. in the direction from the main channel 10 towards the main channel 20/20'. In practice it can be seen that the local increase in cross-section starts from the connection point with the main channel 10 upstream of the bridge channel 31, 31', forming a restriction at or near said connection point.

The embodiment shown in fig. 1 and 2 is characterized in that the channels exhibit an irregular height pattern from one island of plate material to another; that is, there is no discernible regularity in the pattern other than the symmetry imposed by the arrangement of the inlet and outlet (in the case shown, symmetry about a central horizontal axis). Individual islands do not exhibit multiple axes of symmetry and are relatively susceptible to many different island shapes. Some of the islands may have wedge-shaped features directed toward the oncoming flow, resulting in the channel branching into several channels.

Fig. 3 shows a two-dimensional image of a third embodiment of a heat sink according to the present invention.

The heat sink 100 comprises a substantially flat solid plate 101, said solid plate 101 being provided with a plurality of fluid flow channels. A plurality of fluid flow channels are formed to direct coolant from the inlet 110 to the outlet 120 of the plate. In this embodiment the plate is bounded peripherally by impermeable edges, and the inlet 110 and outlet 120 are arranged on the circumference of the plate 101 and provided with attachment points for fluid ducts or the like. Since the inlet 110 and the outlet 120 are arranged on the same side of the plate 101, the coolant essentially turns a U through the plate.

The plurality of channels comprises at least two main channels 10, 20, which are interconnected by at least a plurality of bridge channels 31, -33.

The bridge channels 31-33 have a cross-section which locally increases in the flow direction, i.e. in the direction from the main channel 10 towards the main channel 20 in the figure. In practice it can be seen that the local increase in cross-section starts from the connection point with the main channel 10 upstream of the bridge channels 31-33, forming a restriction at or near said connection point.

It can also be seen that the bridging channels 31-33 are not branched and that they have a locally decreasing cross-section downstream of the locally increasing cross-section in the flow direction. This appears as a second restriction, which is located near the connection point of the main channel 20 downstream of the bridge channels 31-33.

It should be noted that there need not be a single distinct partition of channels in the "main channels" and the "bridge channels", but rather in each embodiment there is at least one such partition (e.g. the partition indicated in the respective figures) which fulfills the requirement that at least two main channels are interconnected by at least a plurality of bridge channels, wherein the bridge channels have a locally increasing cross section in the flow direction.

In all the figures only one inlet and one outlet are shown, but it is equally possible to have more than one inlet and/or more than one outlet. In all the figures the inlet and outlet are shown arranged along the perimeter in the plane of the plate, but it is equally possible to have one or more inlets and/or one or more outlets connected to the main face of the heat sink.

For comparison purposes, fig. 4 illustrates an exemplary heat sink having a serpentine flow channel as known in the prior art. The device relates to a water-cooled aluminium radiator (grey) mounted on a steel plate (black) of thickness 0.002 m. The steel plate has a square shape of 10cm × 10 cm. Providing an inlet on one circumferential edge of the heat sinkThe port 110 and the outlet 120, both having a square cross-section of 1cm x 1 cm. A single serpentine coolant channel extends from the inlet 110 to the outlet 120; the coolant channels are designed to produce the same amount of material as in the heat sink according to the invention shown in fig. 4, i.e. 60.3% material. For the purpose of the present comparative simulation, a uniform water flow velocity of 0.1m/s is applied at the inlet side 110. Inlet (T)in) The coolant temperature at (b) is assumed to be 293K.

The steel plate used was 10kW/m from below2The heat flux of (a) is uniformly heated. The thermal performance of the designs of fig. 4 and 5 is measured at the bottom of the steel plate, which is also the location of the heat source. The design of fig. 4 and 5 is compared as follows:

it can be seen that the average and maximum temperatures of the radiator according to the invention are significantly lower for the same amount of radiator material, the same coolant temperature and velocity at the inlet and the same positioning of the inlet and outlet.

The same applies to the thermal resistance RthSaid thermal resistance RthDefined in terms of inlet temperature Tin, outlet temperature T and total heat input Q (Q qA 10 kW/m)2×0.01m2100W) such that:

Rth=(T–Tin)/Q

the pressure drop observed on the radiator according to the invention is almost an order of magnitude lower than that observed on the radiator according to the prior art; this difference has important technical and economic benefits as it means that a smaller (cheaper) coolant pump can be used to obtain better cooling.

The heat sink according to the invention, in particular the channels in the substantially flat plate, may be produced by milling, laser cutting, etching, 3D printing, sheet metal forming (e.g. die forming and hydroforming) and other known production methods. It is particularly advantageous to design the heat sink 100 according to the present invention such that the plurality of fluid flow channels have a common minimum width, which is suitable for manufacturing techniques.

Fig. 5 shows a specific manufacturing method of the heat sink 100 according to the present invention. The method includes cutting a substantially flat solid sheet 101 of dimension 1010 from a quantity of stock material to obtain a desired shape. Although many heat sinks are rectangular, other shapes are possible. Machining 1020 the plurality of flow channels to a depth of less than the entire thickness of the substantially flat, solid plate, such that the plurality of channels comprises at least two main channels 10, 20 interconnected by at least a plurality of bridge channels 31-37, and such that the bridge channels have a locally increasing cross-section in the flow direction. Finally, a substantially flat cover 102 is placed 1030 onto the machined plate 101.

Although the invention has been described above with reference to specific embodiments, this has been done by way of illustration only, and not by way of limitation, and the scope of the invention should be determined from the appended claims. It should also be noted that the concepts described herein may be applied to heat exchangers with similar effect.

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